Process for preparing polycarbonate using non-cyclic polyamine catalysts

ABSTRACT

An interfacial polymerization process for preparing high molecular weight aromatic polycarbonates by reacting a dihydric phenol with a carbonate precursor in the presence of a catalytic amount of certain non-cyclic polyamines or salts of non-cyclic polyamines.

This invention is directed to an interfacial polymerization process for preparing high molecular weight aromatic polycarbonates which comprises reacting under interfacial polycarbonateforming conditions a dihydric phenol and a carbonate precursor in the presence of a ctalytic amount of a non-cyclic polyamine or a non-cyclic polyamine salt.

BACKGROUND OF THE INVENTION

Polycarbonates are well known thermoplastic materials finding a wide range of uses, particularly for injection molding applications and as glazing sheet for replacement of window glass. The interfacial polymerization technique, which is one of the methods employed in preparing a polycarbonate, involves reacting a dihydric phenol and a carbonate precursor in the presence of an aqueous caustic solution containing an alkali or alkaline earth metal hydroxide, and an inert organic solvent medium which is a solvent for the polycarbonate as it is formed. While the interfacial polymerization process is generally effective in producing polycarbonates, it does, in general, suffer from two disadvantages. Firstly, the rate of reaction is relatively slow. Secondly, there is a general difficulty in producing high molecular weight aromatic polycarbonates, i.e., those having a weight average molecular weight of about 15,000 to greater. Many techniques, such as those employing ultrasonic waves during the reaction, have been employed to remedy these two disadvantages. These techniques have not always proved to be entirely effective and involve the use of cumbersome and expensive equipment. It is advantageous economically to speed up the reaction and to produce high molecular weight aromatic polycarbonates without having to employ extra equipment or more severe reaction conditions. One such method is the use of catalysts in the interfacial polymerization process.

However, there is generally relatively little known about effective catalysis of polycarbonate reactions. The prior art discloses that certain compounds such as tertiary and quaternary amines and their salts (U.S. Pat. No. 3,275,601), guanidine compounds (U.S. Pat. No. 3,763,099), and ammonia and ammonium compounds (U.S. Pat. No. 4,055,544) are effective catalysts for the interfacial polymerization process for producing polycarbonates. However, the prior art also teaches that certain organic nitrogen compounds function as molecular weight regulators or chain terminators in the polycarbonate reactions. Thus, the afore-mentioned U.S. Pat. No. 3,275,601 discloses that aniline and methyl aniline function as chain terminators in the polycarbonate reaction, while U.S. Pat. No. 4,001,184 discloses that primary and secondary amines are effective molecular weight regulators. Furthermore, U.S. Pat. No. 4,111,910 teaches that ammonia, ammonium compounds, primary amines, and secondary amines function as chain terminators in the formation of polycarbonates via the interfacial polymerization process, and U.S. Pat. No. 3,223,678 teaches that monoethanolamine and morpholine act to break the polycarbonate chain thereby resulting in lower molecular weight polycarbonates.

DESCRIPTION OF THE INVENTION

This invention is directed to an interfacial polymerization process for producing high molecular weight aromatic carbonate polymers wherein a dihydric phenol is reacted with a carbonate precursor in the presence of an aqueous caustic solution containing an alkali metal or alkaline earth metal hydroxide and a catalyst which is a non-cyclic polyamine or a salt of a non-cyclic polyamine.

The reaction of a dihydric phenol such as 2,2-bis(4-hydroxyphenyl)propane with a carbonate precursor such as phosgene results in a high molecular weight aromatic polycarbonate polymer consisting of dihydric phenol derived units bonded to one another through carbonate linkages. The reaction is carried out in the presence of an aqueous caustic solution containing the alkali and alkaline earth metal hydroxide as acid acceptors and an inert organic solvent medium which is a solvent for the polycarbonate as it is formed. Generally, a molecular weight regulator is also present to control the molecular weight of the polycarbonate polymer. In the process of the present invention, a polyamine is present and acts as an effective catalyst to speed up the reaction between the carbonate precursor and the dihydric phenol.

The high molecular weight aromatic carbonate polymers produced in accordance with the practice of this invention include carbonate homopolymers of dihydric phenols or carbonate copolymers of two or more different dihydric phenols. Additionally, the production of high molecular weight thermoplastic randomly branched polycarbonates and copolyester-polycarbonates are included within the scope of this invention. The randomly branched polycarbonates are prepared by coreacting a polyfunctional organic compound with the afore-described dihydric phenol and carbonate precursor.

The dihydric phenols employed in the practice of this invention are known dihydric phenols in which the sole reactive groups are the two phenolic hydroxyl groups. Some of these are represented by the general formula ##STR1## wherein A is a divalent hydrocarbon radical containing 1-15 carbon atoms, --S--, --S--S--, ##STR2## X is independently hydrogen, halogen, or a monovalent hydrocarbon radical such as an alkyl group of 1-4 carbons, an aryl group of 6-10 carbons such as phenyl, tolyl, xylyl, naphthyl, a oxyalkyl group of 1-4 carbons or an oxyaryl group of 6-10 carbons and n is 0 or 1.

Typical of some of the dihydric phenols that can be employed in the practice of the present invention are bisphenols such as bis(4-hydroxyphenyl)methane, 2,2-bis(4-hydroxyphenyl)propane (also known as bisphenol-A), 2,2-bis(4-hydroxy-3-methylphenyl)propane, 4,4-bis(4-hydroxyphenyl)heptane, 2,2-bis(4-hydroxy-3,5-dichlorophenyl)propane, 2,2-bis(4-hydroxy-3,5-dibromophenyl)propane, etc., dihydric phenol ethers such as bis(4-hydroxyphenyl)ether, bis(3,5-dichloro-4-hydroxyphenyl)ether, etc.; dihydroxydiphenyls such as p,p'-dihydroxydiphenyl, 3,3'-dichloro-4,4'-dihydroxydiphenyl, etc.; dihydroxyaryl sulfones such as bis(4-hydroxyphenyl)sulfone, bis(3,5-dimethyl-4-hydroxyphenyl)sulfone, etc., dihydroxy benzenes, resorcinol, hydroquinone, halo- and alkyl-substituted dihydroxy benzenes such as 1,4-dihydroxy-2,5-dichlorobenzene, 1,4-dihydroxy-3-methylbenzene, etc., and dihydroxy diphenyl sulfides and sulfoxides such as bis(4-hydroxyphenyl)sulfide and bis(4-hydroxyphenyl)sulfoxide, bis-(3,5-dibromo-4-hydroxyphenyl)sulfoxide, etc. A variety of additional dihydric phenols are also available and are disclosed in U.S. Pat. Nos. 2,999,835, 3,028,365 and 3,153,008, all of which are incorporated herein by reference. It is, of course, possible to employ two or more different dihydric phenols or a copolymer of a dihydric phenol with glycol or with hydroxy or acidterminated polyester, or with a dibasic acid in the event a polycarbonate copolymer or interpolymer rather than a homopolymer is desired for use in the preparation of the polycarbonate polymers of this invention. Also employed in the practice of this invention are blends of any of the above dihydric phenols, the preferred dihydric phenol is bisphenol-A. The polyfunctional organic compounds which may be included within the scope of this invention are set forth in U.S. Pat. Nos. 3,635,895 and 4,001,184, which are incorporated herein by reference. These polyfunctional aromatic compounds contain at least three functional groups which are carboxyl, carboxylic anhydride, haloformyl, or mixtures thereof. Examples of these polyfunctional aromatic compounds include trimellitic anhydride, trimellitic acid, trimellityl trichloride, 4-chloroformyl phthalic anhydride, pyromellitic acid, pyromellitic dianhydride, mellitic acid, mellitic anhydride, trimesic acid, benzophenonetetracarboxylic acid, benzophenonetetracarboxylic anhydride, and the like. The preferred polyfunctional aromatic compounds are trimellitic anhydride or trimellitic acid or their haloformyl derivatives. Also included herein are blends of a linear polycarbonate and a branched polycarbonate.

The carbonate precursor can be either a carbonyl halide or a bishaloformate. The carbonyl halides include carbonyl bromide, carbonyl chloride, and mixtures thereof. The bishaloformates suitable for use include the bishaloformates of dihydric phenols such as bischloroformates of 2,2-bis(4-hydroxyphenyl)propane, 2,2-bis(4-hydroxy-3,5-dichlorophenyl)propane, hydroquinone, and the like, or bishaloformates of glycols such as bishaloformates of ethylene glycol, and the like. While all of the above carbonate precursors are useful, carbonyl chloride, also known as phosgene, is preferred.

By adding monofunctional compounds which are capable of reacting with phosgene or with the end groups of the polycarbonates consisting of the chlorocarbonic acid ester group and which terminate the chains, such as the phenols, e.g., phenol, tert-butylphenyl, cyclohexylphenol, and 2,2-(4,4-hydroxyphenylene-4'-methoxyphenylene)propane, aniline and methylaniline, it is possible to regulate the molecular weight of the polycarbonates.

As mentioned hereinabove, the acid acceptor is an alkali or alkaline earth metal hydroxide. Illustrative of these acid acceptors are sodium hydroxide, lithium hydroxide, potassium hydroxide, calcium hydroxide and the like. The amount of said acid acceptor present should be sufficient to maintain the pH of the aqueous caustic solution above about 9.

Illustrative of the inert organic solvents which are present during the reaction and which dissolve the polycarbonate as it is formed are aromatic hydrocarbons and halogenated hydrocarbons such as benzene, toluene, xylene, chlorobenzene, orthodichlorobenzene, chloroform, methylene chloride, carbon tetrachloride, trichloroethylene and dichloroethane. The solvent is present in an amount effective to solubilize or dissolve substantially all of the polycarbonate as it is formed.

The catalytic compounds useful as catalysts in the process of the instant invention are the non-cyclic polyamines represented by the general formula ##STR3## wherein n is an integer equal to 3-p; p is an integer having a value from 1 to 3, inclusive; m is an integer having a value from 1 to 3, inclusive; R, R¹ and R² are independently selected from hydrogen, alkyl, substituted alkyl, alkenyl, substituted alkenyl, cycloalkyl, substituted cycloalkyl, and aralkyl radicals; W is a divalent aliphatic or cycloaliphatic hydrocarbon radical; and X represents a 5 to 6 membered nitrogen containing heterocyclic radical selected from pyrrole, mono to tetra C₁ to C₅ alkyl substituted pyrrole, pyridine, or mono to tetra C₁ to C₅ alkyl substituted pyridine radicals.

Preferred alkyl radicals are those containing from 1 to about 20 carbon atoms. Illustrative of these preferred alkyl radicals are methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, and the various positional isomers thereof, and likewise the straight and branched chain positional isomers of hexyl, heptyl, octyl, nonyl, decyl, and the like.

Preferred substituted alkyl radicals are those containing from 1 to about 20 carbon atoms and from 1 to about 3 substituent groups independently selected from hydroxyl and alkoxyl groups.

Preferred alkenyl radicals are those containing from 2 to about 20 carbon atoms. Illustrative of these preferred alkenyl radicals are vinyl, propenyl, allyl, butenyl, 2-methylpropenyl, 3-octenyl, and the like.

Preferred substituted alkenyl radicals are those containing from 2 to about 20 carbon atoms and from 1 to about 3 substituent groups independently selected from hydroxyl, alkyl, and alkoxyl radicals.

Preferred cycloalkyl radicals are those containing from 3 to about 14 carbon atoms. Illustrative of these cycloalkyl radicals are cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononly, and the like.

Preferred substituted cycloalkyl radicals are those containing from 3 to about 14 carbon atoms and from 1 to about 3 substituent groups independently selected from lower alkyl, hydroxyl, and alkoxy radicals. Illustrative of these substituted cycloalkyl radicals are hydroxycyclopentyl, 1,2-dimethoxycyclohexyl, and the like.

Preferred aralkyl radicals are those containing from 7 to about 20 carbon atoms. Illustrative of these aralkyl radicals are benzyl, 2-phenylethyl, 2-phenylpropyl, cumyl, naphthylmethyl, naphthylpropyl, and the like.

Preferred divalent aliphatic hydrocarbon radicals represented by W are those containing from 1 to about 14 carbon atoms. Illustrative of these preferred divalent aliphatic hydrocarbon radicals are methylene, ethylene, ethylidene, 1,3-propylene, 1,2-propylene, tetramethylene, hexamethylene, decamethylene, and the like.

Preferred divalent cycloaliphatic hydrocarbon radicals represented by W are those containing from 3 to about 14 carbon atoms. Illustrative of these preferred hydrocarbon radicals are 1,4-cyclohexylene, 1,3-cyclopentylene, 1,5-cyclooctylene, and the like.

Illustrative non-cyclic polyamines represented by Formulae I and II are set forth in Table I.

TABLE I Formula I

N,N'-diethyl-1,4-butanediamine

N,N'-dimethyl-N'-ethyl-1,3-propanediamine

4,7-dimethyltriethylenetetramine

N,N'-di-n-propyl-1,2-propanediamine

N,N'-bis(diethylaminoethyl)-1,3-diaminopropane

3,3'-bis(ethylamino)-N-ethyl dipropylamine

N,N'-dibenzyl ethylenediamine

4,4'-dimethyl cyclohexylenediamine

N,N',N"-trimethyl dihexamethylenetriamine

1,1,7,7-tetramethyl diethylenetriamine

1,1,4-trimethyl diethylenetriamine

bis(dimethylamino)methane

N-(3-aminopropyl)ethylenediamine

tris-(2-aminoethyl)amine

N,N'-dipentyl-1,6-hexanediamine

N,N'-di-tert-butyl ethylenediamine

4,4'-trimethylenedipiperidine

3,3'-iminobispropylamine

2,5-dimethyl-2,5-hexanediamine

triethylenetetramine

di-isopropylamino ethylamine

dimethylamino isopropylamine

tetraethylenepentamine

tetraethyl putrescin

N,N', N"-trimethyl dihexamethylenetriamine

1,1,4,7,10,10-hexamethyl triethylenetetramine

N-ethyl-N,N',N"-trimethyl ethylenediamine

Formula II

2(2-n-propylaminoethyl)pyridine

2,6-bis(2-isopropylaminoethyl)pyridine

The salts of the non-cyclic polyamines represented by Formula I are represented by the general formula ##STR4## while the salts of the non-cyclic polyamines represented by Formula II are represented by the general formula ##STR5## wherein R, R¹, R², W, X, m, n and p are as defined above; Y is a z valent anion, preferably one selected from the group consisting of sulfate, sulfite, phosphite, phosphate, halides, nitrate, nitrite, carbonate, and carboxylates; z is an integer having a value of from 1 to 3, inclusive; a is an integer representative of the valence of the polyamine cation and is the sum of b+pmb¹, preferably a is an integer having a value of from 1 to 4, inclusive; and b and b¹ are independently 0 or 1, provided that one of b or b¹ is 1.

Some illustrative salts of the non-cyclic amines represented by Formula III are set forth in Table II.

TABLE III

4,4'-bipiperidine dihydrochloride

methylenediamine dinitrate

spermidine trihydrochloride

spermine tetrahydrochloride

tetramethylenediamine dihydrochloride

N,N'-dibenzyl ethylenediamine dihydrochloride

These non-cyclic polyamines and their salts are known compounds whose chemistry and prepration are well known to those skilled in the art.

The amount of the catalyst present during the reaction is a catalytic amount. By catalytic amount is meant an amount effective to catalyze the reaction between the dihydric phenol and the carbonate precursor to produce the polycarbonate. Generally, this amount ranges from about 0.01 to about 10 weight percent based on the weight of the dihydric phenol present.

The present process is carried out by reacting the dihydric phenol, such as bisphenol-A, with a carbonate precursor, such as phosgene, in a reaction medium consisting of an aqueous caustic solution and an inert organic solvent for the polycarbonate and in the presence of a catalytic amount of the non-cyclic polyamine or non-cyclic polyamine salt catalyst.

The temperature at which this reaction proceeds may vary from below 0° C. to about 100° C. The reaction proceeds satisfactorily at temperatures ranging from about room temperature to about 50° C. Since the reaction is exothermic, the rate of carbonate precursor addition may be used to control the reaction temperature. The amount of carbonate precursor, such as phosgene, required will generally depend upon the amount of dihydric phenol present. Generally, one mole of the carbonate precursor will react with one mole of dihydric phenol to provide the polycarbonate. When a carbonyl halide, such as phosgene, is used as the carbonate precursor, two moles of hydrohalic acid such as HCl are produced by the above reaction. These two moles of acid are neutralized by the alkali and alkaline earth metal hydroxide acid acceptor present. The foregoing are herein referred to as stoichiometric or theoretical amounts.

PREFERRED EMBODIMENT OF THE INVENTION

In order to more fully and clearly illustrate the present invention, the following examples are presented. It is intended that the examples be considered as illustrative rather than limiting the invention disclosed and claimed herein. In the examples, all parts and percentages are on a weight basis unless otherwise specified.

EXAMPLE 1

This example illustrates an unsuccessful attempt to prepare a high molecular weight aromatic polycarbonate polymer via the interfacial polymerization technique without the presence of a catalyst. To a reactor fitted with a reflux condenser and a mechanical agitator, charge 57 parts of 2,2-bis(4-hydroxyphenyl)propane, 157 parts of water, 325 parts of methylene chloride, and 1.2 parts of para-tertiarybutylphenol. Phosgene is then added to the reaction mixture at a rate of 0.65 parts per minute for a period of 30 minutes while maintaining the pH at 9 by the addition of a 15% aqueous sodium hydroxide solution. After 30 minutes, the pH is raised to 11.0 by the use of additional amounts of sodium hydroxide solution. Phosgenation is continued for a further 10 minutes at this pH. The material is recovered from the reaction and found to have an intrinsic viscosity of 0.12 dl./g. This indicates that no practical degree of polymerization is achieved.

EXAMPLE 2

This example illustrates a successful preparation of a high molecular weight aromatic polycarbonate polymer via the interfacial polymerization technique in the presence of diamine catalyst. To a reactor fitted with a reflux condenser and a mechanical agitator, charge 57 parts of 2,2-bis(4-hydroxyphenyl)propane, 157 parts of water, 325 parts of methylene chloride, and 0.52 part of N,N'-dimethyl-1,3-propanediamine. Phosgene is then added to the reaction mixture at a rate of 0.65 parts per minute for a period of 30 minutes while maintaining the pH at 9 by the addition of a 15% aqueous sodium hydroxide solution. After 30 minutes, the pH is raised to 11.0 by the use of additional amounts of sodium hydroxide solution. Phosgenation is continued for a further 10 minutes at this pH. The material is recovered from the reaction and found to have an intrinsic viscosity of 0.32 dl./g. This value indicates that a high degree of polymerization is achieved, i.e., a high molecular weight aromatic polycarbonate is produced.

EXAMPLES 3-9

The procedure of Example 2 is substantially repeated, except that the various non-cyclic diamines were substituted for the N,N'-dimethyl-1,3-propanediamine of Example 2. These non-cyclic diamines, the amount of said non-cyclic diamines used, and the intrinsic viscosity of the high molecular weight aromatic polycarbonate polymer formed are set forth in Table III.

                  TABLE III                                                        ______________________________________                                         Ex-                          Parts by Intrinsic                                am-                          Weight of                                                                               Viscosity                                ple  Catalyst       Formula  Catalyst Used                                                                           dl./g.                                   ______________________________________                                         3    N,N-dimethyl-hexa-                                                                            I        0.72     0.31                                          methylenediamine                                                          4    4,4'-bipiperidine                                                                             III      1.2      0.37                                          dihydrochloride                                                           5    diethylenetriamine                                                                            I        0.52     0.27                                     6    triethylenetetramine                                                                          I        0.73     0.30                                     7    1,3-di(4-pyridyl)pro-                                                                         II       0.47      0.283                                        pane                                                                      8    2(2-n-propylamino-                                                                            II       0.42     0.36                                          ethyl)pyridine                                                            9    N,N'-di-tertiary-                                                                             I        0.86     0.27                                          butylethylenediamine                                                      ______________________________________                                    

As can be seen by a comparison of Example 1 with Examples 2-9, the use of the catalysts of the instant invention results in the production of high molecular weight aromatic polycarbonates via the interfacial polymerization technique, while in the absence of a catalyst the interfacial polymerization process is generally ineffective in producing a high molecular weight aromatic polycarbonate under substantially identical reaction conditions.

It will thus be seen that the objects set forth above, among those made apparent from the preceding description, are efficiently attained, and since certain changes may be made in carrying out the above process and the composition set forth without departing from the scope of the invention, it is intended that all matters contained in the above description shall be interpreted as illustrative and not in a limiting sense. 

What I claim is:
 1. An interfacial polymerization process for preparing high molecular weight aromatic polycarbonates which comprises reacting, under interfacial polycarbonate-forming conditions, a dihydric phenol with a carbonate precursor in the presence of a catalytic amount of a non-cyclic polyamine of the formula ##STR6## and its acid addition salts, or a non-cyclic polyamine of the formula ##STR7## and its acid addition salts wherein n is an integer equal to 3-p; p is an integer having a value from 1 to 3, inclusive; m is an integer having a value from 1 to 3, inclusive; R, R¹ and R² are independently selected from the group consisting of hydrogen, alkyl, substituted alkyl, alkenyl, substituted alkenyl, cycloalkyl, substituted cycloalkyl, and aralkyl radicals; W is selected from the group consisting of divalent aliphatic and cycloaliphatic radicals; and X is a 5 to 6 membered nitrogen-containing heterocyclic radical selected from the group consisting of pyrrole, mono to tetra C₁ to C₅ alkyl substituted pyrrole, pyridine, and mono to tetra C₁ to C₅ alkyl substituted pyridine radicals.
 2. The process of claim 1 wherein said catalyst in a non-cyclic polyamine.
 3. The process of claim 2 wherein said dihydric phenol is bisphenol-A, said carbonate precursor is phosgene and the non-cyclic polyamine is that of Formula
 1. 4. The process of claim 3 wherein said non-cyclic polyamine is present in an amount from about 0.01 to about 10 weight percent based on the weight of bisphenol-A.
 5. The process of claim 2 wherein said non-cyclic polyamine is that of formula
 1. 6. The process of claim 5 wherein said dihydric phenol is bisphenol-A and said carbonate precursor is phosgene.
 7. The process of claim 6 wherein said non-cyclic polyamine is present in an amount of from about 0.01 to about 10 weight percent based on the weight of said bisphenol-A.
 8. The process of claim 1 wherein said catalyst is a salt of a non-cylic polyamine.
 9. The process of claim 8 wherein said salt of a non-cyclic polyamine is a salt of a Formula 2 compound.
 10. The process of claim 8 wherein said salt of a polyamine is a salt of a Formula 1 compound.
 11. The process of claim 10 wherein said dihydric phenol is bisphenol-A and said carbonate precursor is phosgene.
 12. The process of claim 11 wherein said salt of a non-cyclic polyamine is present in an amount of from about 0.01 to about 10 weight percent based on the weight of bisphenol-A.
 13. The process of claim 9 wherein said dihydric phenol is bisphenol-A and said carbonate precursor is phosgene.
 14. The process of claim 13 wherein said salt of a non-cyclic polyamine is present in an amount of from about 0.01 to about 10 weight percent based on the weight of bisphenol-A. 